DE102005034941B4 - Reformer for the production of synthesis gas - Google Patents
Reformer for the production of synthesis gas Download PDFInfo
- Publication number
- DE102005034941B4 DE102005034941B4 DE102005034941A DE102005034941A DE102005034941B4 DE 102005034941 B4 DE102005034941 B4 DE 102005034941B4 DE 102005034941 A DE102005034941 A DE 102005034941A DE 102005034941 A DE102005034941 A DE 102005034941A DE 102005034941 B4 DE102005034941 B4 DE 102005034941B4
- Authority
- DE
- Germany
- Prior art keywords
- gas
- channels
- fuel
- reformer
- oxidizer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/386—Catalytic partial combustion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/432—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
- B01F25/4323—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa using elements provided with a plurality of channels or using a plurality of tubes which can either be placed between common spaces or collectors
- B01F25/43231—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa using elements provided with a plurality of channels or using a plurality of tubes which can either be placed between common spaces or collectors the channels or tubes crossing each other several times
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
- B01J8/0221—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical shaped bed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0278—Feeding reactive fluids
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
- H01M8/0625—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material in a modular combined reactor/fuel cell structure
- H01M8/0631—Reactor construction specially adapted for combination reactor/fuel cell
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
- C01B2203/0261—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a catalytic partial oxidation step [CPO]
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
- C01B2203/066—Integration with other chemical processes with fuel cells
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1205—Composition of the feed
- C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
- C01B2203/1235—Hydrocarbons
- C01B2203/1247—Higher hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1276—Mixing of different feed components
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1276—Mixing of different feed components
- C01B2203/1282—Mixing of different feed components using static mixers
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1288—Evaporation of one or more of the different feed components
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Abstract
Reformer
zum Erzeugen eines wasserstoffhaltigen Synthesegases (15) aus einem
Brennstoff (6) und aus einem Oxidator (9), insbesondere für eine Brennstoffzellenanlage
(16),
– mit
einer Brennstoffzuführeinrichtung
(2) zum Zuführen eines
gasförmigen
Brennstoffs (6),
– mit
einer Oxidatorzuführeinrichtung
(3) zum Zuführen
eines gasförmigen
Oxidators (9),
– mit
einem Reaktor (4) zum Erzeugen des Synthesegases (15) aus dem Brennstoff
(6) und aus dem Oxidator (9),
– wobei stromauf des Reaktors
(4) eine Mischeinrichtung (5) angeordnet ist, die einen von Gasen
durchströmbaren Körper (10)
aufweist,
– wobei
der Körper
(10) zwischen einer im Betrieb des Reformers (1) mit dem Brennstoffgas
(6) und mit dem Oxidatorgas (9) beaufschlagten Einströmseite (11)
und einer Ausströmseite
(12), aus der im Betrieb des Reformers (1) ein aus Brennstoffgas
(6) und Oxidatorgas (9) gebildetes Gasgemisch (14) ausströmt, wenigstens
eine im Strömungsweg
angeordnete, für
Gase durchlässige,
poröse Wandung
(13) aufweist,
– wobei
der Körper...Reformer for generating a hydrogen-containing synthesis gas (15) from a fuel (6) and from an oxidizer (9), in particular for a fuel cell system (16),
With a fuel supply device (2) for supplying a gaseous fuel (6),
With an oxidizer supply device (3) for supplying a gaseous oxidizer (9),
With a reactor (4) for generating the synthesis gas (15) from the fuel (6) and from the oxidizer (9),
Wherein a mixing device (5) is arranged upstream of the reactor (4) and has a body (10) permeable by gases,
- wherein the body (10) between a in the operation of the reformer (1) with the fuel gas (6) and with the oxidant gas (9) acted upon inflow side (11) and an outflow side (12), from which in the operation of the reformer (1) a gas mixture (14) formed from fuel gas (6) and oxidizer gas (9) flows out, has at least one porous wall (13) which is arranged in the flow path and permeable to gases,
- where the body ...
Description
Die vorliegende Erfindung betrifft einen Reformer zum Erzeugen eines wasserstoffhaltigen Synthesegases aus einem Brennstoff und aus einem Oxidator, insbesondere für eine Brennstoffzellenanlage. Die Erfindung betrifft außerdem eine neuartige Verwendung eines von Gasen durchströmbaren Körpers.The The present invention relates to a reformer for producing a hydrogen-containing synthesis gas from a fuel and from an oxidizer, especially for a fuel cell system. The invention also relates to a novel use of a body through which gases can flow.
Moderne Kraftfahrzeuge können zur Deckung ihres Stromverbrauchs mit einer motorunabhängig arbeitenden Stromerzeugereinrichtung ausgestattet sein, die mit einer Brennstoffzelle betrieben wird. Hierbei wird mit Hilfe eines Reformers aus dem jeweils zur Verfügung stehenden Kraftstoff, wie z. B. Benzin oder Diesel oder Methangas, ein wasserstoffhaltiges Brennstoffgas oder Synthesegas als Reformat hergestellt. Dieses Synthesegas kann dann in einer Brennstoffzelle zusammen mit einem gasförmigen sauerstoffhaltigen Oxidator, in der Regel Luft, zur Erzeugung von Strom genutzt werden. Zur Erzeugung des Synthesegases arbeitet der Reformer mit einem Reaktor, der in der Regel durch einen Katalysator gebildet ist, der so ausgestaltet ist, dass er bei einem stark unterstöchiometrischen Betrieb (Brennstoffüber schuss) den Brennstoff nur partiell oxidiert, wodurch unter anderem molekularer Wasserstoff entsteht.modern Motor vehicles can to cover their power consumption with a motor-independent working Generator device to be equipped with a fuel cell is operated. This is done with the help of a reformer from the respective to disposal standing fuel, such as. As gasoline or diesel or methane gas, a hydrogen-containing fuel gas or synthesis gas as a reformate produced. This syngas can then be in a fuel cell together with a gaseous oxygen-containing oxidizer, usually air, for the production of Electricity can be used. To generate the synthesis gas works the Reformer with a reactor, usually by a catalyst is formed, which is designed so that it is in a highly substoichiometric Operation (fuel surplus) the fuel is only partially oxidized, causing, inter alia, molecular Hydrogen is produced.
Aus
der
Bei
der
Bei
der
Die
Grundsätzlich kann besagter Körper denselben Aufbau aufweisen wie ein an sich bekanntes keramisches Partikelfilter mit wechselseitig verschlossenen Einlasskanälen und Auslasskanälen, die über gemeinsame, gasdurchlässige, poröse Wandungen voneinander getrennt sind. Somit nutzt und verallgemeinert die vorliegende Erfindung den Gedanken, ein Partikelfilter zur Homogenisierung einer Gasströmung zu verwenden.Basically said body have the same structure as a ceramic known per se Particle filter with mutually closed inlet channels and exhaust ports, the over common, gas-permeable, porous Walls are separated from each other. Thus uses and generalizes the present invention the idea of a particle filter for homogenization a gas flow to use.
Neben der Homogenisierung des dem Reaktor zugeführten Gasgemischs bietet der stromauf des Reaktors angeordnete Körper zusätzlich den Vorteil, dass Partikel, in der Regel Ruß, die bei bestimmten Betriebszuständen des Reformers, stromauf des Reaktors entstehen können, durch den Körper aus der Gasströmung heraus gefiltert werden können. Die porösen Wandungen halten die mitgeführten Partikel zurück. Der Körper der Mischeinrichtung arbeitet dann zusätzlich als Partikelfilter. Hierdurch kann der Reaktor vor einer schädlichen Verschmutzung geschützt werden.Next the homogenization of the gas mixture supplied to the reactor offers the bodies arranged upstream of the reactor additionally have the advantage that particles, usually soot, in certain operating conditions of the reformer, upstream of the reactor can emerge through the body the gas flow can be filtered out. The porous ones Walls hold the entrained Particles back. The body the mixing device then also works as a particle filter. As a result, the reactor can be protected from harmful contamination.
Weitere wichtige Merkmale und Vorteile der Erfindung ergeben sich aus den Unteransprüchen, aus den Zeichnungen und aus der zugehörigen Figurenbeschreibung anhand der Zeichnungen.Further important features and advantages of the invention will become apparent from the Dependent claims, from the drawings and from the associated description of the figures the drawings.
Es versteht sich, dass die vorstehend genannten und die nachstehend noch zu erläuternden Merkmale nicht nur in der jeweils angegebenen Kombination, sondern auch in anderen einander kommunizieren. In die porösen Wandungen ist ein Katalysator integriert.It it is understood that the above and the following yet to be explained features not only in the specified combination, but also in communicate with each other. In the porous walls is a catalyst integrated.
Aus
der
Aus
der
Aus
der
Schließlich betrifft
die
Für eine ordnungsgemäße und effektive Funktion des Reaktors ist dabei entscheidend, dass das zugeführte Brennstoff-Oxidator-Gasgemisch möglichst homogen ist.For a proper and effective function of the reactor is crucial that the supplied fuel-oxidizer gas mixture possible is homogeneous.
Hier setzt die vorliegende Erfindung an. Die Erfindung beschäftigt sich mit dem Problem, für einen Reformer der eingangs genannten Art eine verbesserte Ausführungsform anzugeben, die sich insbesondere durch eine homogene Gasgemischzuführung zum Reaktor auszeichnet. Darüber hinaus beschäftigt sich die Erfindung allgemein mit dem Problem, für die Durchmischung von wenigstens zwei Gasen einen vorteilhaften Weg aufzuzeigen.Here uses the present invention. The invention is concerned with the problem, for a reformer of the type mentioned an improved embodiment specify, in particular by a homogeneous gas mixture supply to Characterized reactor. About that busy the invention generally with the problem for the mixing of at least two gases to show an advantageous way.
Diese Probleme werden durch die Gegenstände der unabhängigen Ansprüche gelöst. Vorteilhafte Ausführungsformen sind Gegenstand der abhängigen Ansprüche.These Problems are solved by the subject matters of the independent claims. advantageous embodiments are the subject of the dependent Claims.
Die Erfindung beruht auf dem allgemeinen Gedanken, einen von Gasen durchströmbaren Körper, der zwischen einer Einströmseite und einer Ausströmseite zumindest eine im Strömungsweg angeordnete, für Gase durchlässige, poröse Wandung aufweist, zum Vermischen der Brennstoffgasströmung mit der Oxidatorgasströmung zu verwenden. Hierzu wird besagter Körper stromauf des Reaktors angeordnet und dient dort als Mischeinrichtung. Es hat sich gezeigt, dass inhomogene Gasströmungen bei Kombinationen oder in Alleinstellung verwendbar sind, ohne den Rahmen der vorliegenden Erfindung zu verlassen.The The invention is based on the general idea, a permeable body of gases, the between an inflow side and an outflow side at least one in the flow path arranged, for Gases permeable, porous Wall, for mixing the fuel gas flow with the oxidizer gas flow to use. For this purpose, said body is arranged upstream of the reactor where it serves as a mixing device. It has been shown that inhomogeneous Gas flows in combinations or used alone, without the scope of the present To leave invention.
Bevorzugte Ausführungsbeispiele der Erfindung sind in den Zeichnungen dargestellt und werden in der nachfolgenden Beschreibung näher erläutert, wobei sich gleiche Bezugszeichen auf gleiche oder ähnliche oder funktional gleiche Bauteile beziehen.preferred embodiments The invention are illustrated in the drawings and in the following description explains where like reference numerals refer to the same or similar or functionally identical components relate.
Es zeigen, jeweils schematisch,It show, in each case schematically,
Entsprechend
Die
Oxidatorzuführeinrichtung
Die
Mischeinrichtung
Das
homogene Gasgemisch
Zweckmäßig bildet
der Reformer
Optional
kann die Brennstoffzellenanlage
Entsprechend
Entsprechend
den
Im
Unterschied dazu zeigt
Bei
diesen Ausführungsformen
beruht die Durchmischung auch auf dem Effekt, dass die Gasströme mehrerer
Einlasskanäle
Entsprechend
den
Bei
der in
Die
mit Bezug auf die
Die
porösen
Wandungen
Mit
Hilfe des hier vorgestellten Körpers
Darüber hinaus
ergeben sich bei der beschriebenen bevorzugten Anwendung des Körpers
Auch
während
des normalen Reformerbetriebs kann es zu einer Partikelbildung bzw.
Rußbildung
bereits stromauf der Mischeinrichtung
Beim
Abschalten des Reformers
Für die Regeneration
des zusätzlich
als Partikelfilter dienenden Körpers
Claims (8)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102005034941A DE102005034941B4 (en) | 2005-07-22 | 2005-07-22 | Reformer for the production of synthesis gas |
EP06011334A EP1745843A1 (en) | 2005-07-22 | 2006-06-01 | Reformer for the generation of synthesis gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102005034941A DE102005034941B4 (en) | 2005-07-22 | 2005-07-22 | Reformer for the production of synthesis gas |
Publications (2)
Publication Number | Publication Date |
---|---|
DE102005034941A1 DE102005034941A1 (en) | 2007-02-01 |
DE102005034941B4 true DE102005034941B4 (en) | 2008-12-18 |
Family
ID=37129140
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE102005034941A Expired - Fee Related DE102005034941B4 (en) | 2005-07-22 | 2005-07-22 | Reformer for the production of synthesis gas |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP1745843A1 (en) |
DE (1) | DE102005034941B4 (en) |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0334710B1 (en) * | 1988-03-16 | 1992-04-22 | Institut Français du Pétrole | Oxidation process for a gaseous phase oxidizable charge and the reactor for carrying it out |
DE3875305T2 (en) * | 1987-08-14 | 1993-02-25 | Davy Mckee Corp | GAS MIXER AND DISTRIBUTOR FOR A REACTOR. |
DE10130945A1 (en) * | 2000-06-28 | 2002-03-28 | Toyota Motor Co Ltd | Fuel reforming device and method for controlling the fuel reforming device |
DE10028865A1 (en) * | 2000-06-10 | 2002-04-18 | Xcellsis Gmbh | Device for the catalytic generation of hydrogen from hydrocarbons |
DE10151519A1 (en) * | 2001-10-18 | 2003-05-08 | Ballard Power Systems | Reactor used for a fuel cell arrangement in a gas producing system in vehicles has a porous material arranged between inflow and catalyst regions and between outflow and a catalyst regions |
DE10247540A1 (en) * | 2001-10-15 | 2003-05-28 | Gen Motors Corp | Reactor systems with a foam to suppress autoignition and carbon formation |
DE10230149A1 (en) * | 2002-07-04 | 2004-02-12 | Sgl Acotec Gmbh | Method and device for producing hydrogen |
DE10343811A1 (en) * | 2002-09-27 | 2004-04-08 | General Motors Corp., Detroit | Device for retaining by-product connections for a burner operated in the fuel-rich starting phase |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3572395B2 (en) * | 2000-02-18 | 2004-09-29 | 日産自動車株式会社 | Combustor for fuel reformer |
US7122170B2 (en) * | 2000-07-25 | 2006-10-17 | Conocophillips Company | Catalysts for SPOC™ enhanced synthesis gas production |
JP4830197B2 (en) * | 2000-09-13 | 2011-12-07 | トヨタ自動車株式会社 | Fuel reformer |
JP2004011933A (en) * | 2002-06-03 | 2004-01-15 | Nissan Motor Co Ltd | Combustor, fuel reformer, and fuel cell system |
-
2005
- 2005-07-22 DE DE102005034941A patent/DE102005034941B4/en not_active Expired - Fee Related
-
2006
- 2006-06-01 EP EP06011334A patent/EP1745843A1/en not_active Withdrawn
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3875305T2 (en) * | 1987-08-14 | 1993-02-25 | Davy Mckee Corp | GAS MIXER AND DISTRIBUTOR FOR A REACTOR. |
EP0334710B1 (en) * | 1988-03-16 | 1992-04-22 | Institut Français du Pétrole | Oxidation process for a gaseous phase oxidizable charge and the reactor for carrying it out |
DE10028865A1 (en) * | 2000-06-10 | 2002-04-18 | Xcellsis Gmbh | Device for the catalytic generation of hydrogen from hydrocarbons |
DE10130945A1 (en) * | 2000-06-28 | 2002-03-28 | Toyota Motor Co Ltd | Fuel reforming device and method for controlling the fuel reforming device |
DE10247540A1 (en) * | 2001-10-15 | 2003-05-28 | Gen Motors Corp | Reactor systems with a foam to suppress autoignition and carbon formation |
DE10151519A1 (en) * | 2001-10-18 | 2003-05-08 | Ballard Power Systems | Reactor used for a fuel cell arrangement in a gas producing system in vehicles has a porous material arranged between inflow and catalyst regions and between outflow and a catalyst regions |
DE10230149A1 (en) * | 2002-07-04 | 2004-02-12 | Sgl Acotec Gmbh | Method and device for producing hydrogen |
DE10343811A1 (en) * | 2002-09-27 | 2004-04-08 | General Motors Corp., Detroit | Device for retaining by-product connections for a burner operated in the fuel-rich starting phase |
Also Published As
Publication number | Publication date |
---|---|
EP1745843A1 (en) | 2007-01-24 |
DE102005034941A1 (en) | 2007-02-01 |
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